Method for the preparation of composite pigments



' oxide, either barium or calcium sulfate.

Patented Oct. 24, 1939 PATENT OFFICE LIETHOD FOR THE PREPARATION OF COMPOSITE PIGMENTS Hugh V. Alessandroni, New York, N. Y., assignor,

by memo assignments, to National LeadCompany, New York, N. Y., a corporation of New Jersey No Application A!!! 24, 1935, Serial No. 37,715

3: Claims. (01. 134-50 My invention relates to novel methods for the manufacture of pigments, particularly to the manufacture of that type of pigment known as "composite" in which a primary pigment is intimately associated with one or more secondary pigments.

The objects of my invention include novel methods for the manufacture of composite pigments which methods possess many advantages over those oi the prior art.

Pigments are said to be of the composite type when they consist of two or more individual components. Thus, lithopone, a zinc sulfide-barium sulfate composition, is a composite pigment. So also are. the well-known, so-called coalesced composite titanium dioxide pigments of the prior art in which there is present beside titanium di- 1- tanated lithopone, a tertiary pigment composed oi. titanium dioxide, zinc sulfide and barium sulfate is also of the composite type. In all composite pigments there is present at least one material which may be regarded as the primary pigment. Such a material possesses relatively good pigment properties such as, for example, tinting strength,-hiding power, opacity, etc. In addition to the primary pigment there is also present in composite pigments at least one other material which may be regarded as a secondary pigment. Such a material possesses pigme nt properties relatively inferior to those of the primary pigment In composite pigments the function of the secondary pigment is referred to as that of an extender, a carrier" or "diluent for the primary pigment, although, in the present invention, the secondary pigment may itself possess definite pigment properties.

By primary pigment" as used by me to desig-- nate a component of a composite pigment prepared according to the herein described method, I refer to that component which possesses superior pigment properties as compared with the other component or components of the composite pigment and which, whether it be a simple or composite material, is dispersed as a simple material in one suspension. Thus, the primary plg ment component may consist of a simple material such as titanium dioxide, zinc sulfide, or it may consist of a coprecipitated composite pigment prepared by prior art methods. Conversely, "secondary pigment as used by me indicates the component or components of a composite pigment prepared according to the present invention which possesses pigment properties interior to those possessed by the primary pigment constituent. The term "secondary pigmen as used by me would thus include not only the so-called extenders, e. g. barium sulfate, calcium sulfate, asbestine, etc., but also certain other materials possessing relatively good pigment properties, e. g. basic lead carbonate, zinc oxide, etc., when these latter are used in conjunction with a material having even better pigment properties as, for example, titanium dioxide, zinc sulfide, etc.

, For the most part, composite pigments have been prepared in the past by methods which involve a copreclpitation oi the primary and secondary pigments and a subsequent mutual calcination. Lithopone, for example, is prepared by a double decomposition reaction which occurs when solutions of zinc sulfate and barium sulfide are' brought together. The resulting precipitate of zinc sulfide and barium sulfate is then calcined. Composite titanium dioxide pigments are generally prepared by one of two alternative procedures: (1) by adding the secondary pigment, e. g. barium or calcium sulfate, to a titanium solution and precipitating the titaniumoxygen compounds by hydrolysis; or, (2) by adding a solution of a salt, the sulfate of which constitutes the secondary pigment, e. g. calcium or barium chloride, to a titanium sulfate solution thus forming the secondary pigment, in situ, and then precipitating the titanium-oxygen compounds by hydrolysis. The mixed precipitates of titanium-oxygen compounds and secondary pigment are then calcined together. Such methods produce pigments concerning which it has been said that the titanium dioxide is precipitated on and coalesced with the secondary pigment.

Among the reasons for this final or penultimate calcination step may be mentioned the following: (a) to effect changes primarly in the crystalline structure oi certainof the components of the pigment; (b) to eflect or complete a coalescence between the primary and secondary constituents of the composite pigment; (c) to dehydrate one or more of the constituents, if they exist in the coprecipitated mixture as hydroxides or hydrates, etc.; (d) to eliminate volatile impurities.

As a result of this calcination, the pigment properties of the primary pigment, such as tinting strength, covering power, etc., are developed to an optimum degree. The secondary pigment, on the other hand, is essentially unaltered and unimproved. It is evident, therefore, that the prior art methods involve considerable unnecesany treatment of the secondary pigment and, as a consequence of this unnecessary treatment, increased manufacturing costs.

I have now discovered novel methods whereby composite pigments such as those comprising a primary pigment and one or more secondary pigments may be prepared without the necessity of restoring to coprecipitation and mutual calcination. My novel methods are particularly suited to the preparation of composite pigments superior to those manufactured by prior art methods and at a much lower cost of production. These novel methods comprise the coflocculatlon of a mixture consisting of a dispersed suspension of a primary pigment and separately-dispersed suspensions of one or more secondary pigments after which the coflocculated composite pigment is washed, dried and pulverized.

By the term "coflocculation as used by me throughout this description of my invention, I mean the mutual coagulation and integration of pigment particles from a mixture consisting of a dispersed aqueous suspension of a primary pigment and one or more separately-dispersed aqueous suspensions of secondary pigments.

My novel coflocculation methods of preparing composite pigments are clearly distinguished from prior art precipitation methods for preparing composite pigments.

In methods involving precipitation, substances in substantially molecular solution undergo, under suitable conditions, physico-chemical changes which result in the formation of a second, usually diflicultly soluble, phase. other hand, involves only the integration or coagulation of small particles of a dispersed substance to larger particles or flocs. In the former phenomenon the molecules are said to be condensed to minute ultramicroscopic crystals from which in turn larger particles are developed by what is known as grain-growth. In the latter phenomenon particles which may even be so small as to approach colloidal dimension are integrated to larger, visible, macroscopic flocs. In the former the larger particles result from a physico-chemical interaction between the ultramicroscopic crystals and the surrounding solution while in the latter the larger particles result merely from an integration and adherence of a number of smaller particles. Whereas, precipitation implies the transition of substances from the solution phase, through the colloidal phase to the solid phase; flocculation, as used by me, implies merely an agglomeration of small particles to form larger ones.

Hydrolysis, with the formation of hydrous oxides, and double decomposition or metathesis, with the formation of insoluble salts, are typical condensation reactions involving precipitation. Thus, for example, hydrous titanium oxide is formed by hydrolysis of a titanyl sulfate solution while barium sulfate is formed by a double desoluble sulfate.

In practicing my invention, a dispersed suspension of the primary pigment is first prepared by means of a dispersing agent. Separate individual suspensions of the secondary pigment or pigments are prepared, also by means of dispersing agents. These suspensions are then mixed and coflocculation accomplished by one of two procedures: (1) by means of an added coagulating agent; (2) as a result of an interaction between the dispersing agent selected for the primary pigment and the dispersing agent or agents selected for the secondary pigment or pigments.

The dispersion of the primary and Secondary Flocculation, on the I certain emulsifying agents such as pigments may conveniently be eflected by grinding or milling the individual pigment with a suitable quantity of water, for example, a quantity equal in weight to that of the pigment. The dispersing agent may be contained in the water, either in solution, if it be water-soluble, or in suspension, ii it be insoluble in water; or it may be added prior to or during the milling or grinding operation, as desired.

The function of a dispersing agent is not completely understood. It is believed that the disintegration of aggregates of primary particles which results from the use of a suitable dispersing agent is due to a strong, usually preferential absorption of ions. It has been suggested that through the use of such an agent a similar elec-- trical charge is impinged upon the individual particles of the dispersed or suspended substance, the eflect of which is to set up a mutual repulsion between the individual particles, thus preventing coagulation. Furthermore, a dispersing agent may efiect a reduction in the size of the particles of a dispersed or suspended material by partially dissolving them. A substance may also function as a dispersing agent, although with obvious limited application, if it succeeds in nullifying or destroying the agglomerating eifect 01 some other substance present in the material.

Although these general hypotheses are not conclusive, they furnish, in many instances, a guide to the proper selection of the dispersing agents to be employed in the practice of my invention.

Among the materials which exert a. dispersing efl'ect on various primary and secondary pigments and which are, therefore, useful in the practice of my invention may be mentioned: the carbonates and hydroxides of alkali metals, e. g. NaOH, NazCOa, KzCOs; ammonium hydroxide, NH4OH; alkali metal silicates, e. g. NazSiOz; sultides, e. g. H23, certain inorganic salts, e. g. PbClz and BaClz; acidic halides of tri-and tetravalent elements, e. g. Fe, Th, Tl, Ce, Al, Ti, Zr, etc.; metallic soaps, e. g. those of oleic, stearic, palmltic or lauric acid; the ammonium soaps of suli'onated aliphatic oils, e. g. the ammonium soap of suli'onated castor oil; sulfonated fatty oils or acids, e. g. Turkey red oil; alkyl-substituted aryl sulfonlc acids and their salts, e. g. isopropylnaphthalene sulfonic acid and the sodium salt thereof; saponin, tri hydroxyethylamine, etc.

According to the first alternative method or my invention, any suitable dispersing agents may be employed in preparing the dispersed suspension of primary pigment and that 01' the secondary pigment or pigments, and coflocculation may be brought about by the addition, to the mixed suspensions, of a coagulating agent, for example, magnesium sulfate. Strongly acidic or basic substances such as sulfuric acid or sodium hydroxide are often effective as coagulating agents.

It will be readily seen that the selection of a suitable coagulating agent will be determined largely from a consideration of the factors involved in preparing the dispersed suspensions. When added to mixed suspensions which are in a stable condition, it should function in a manner similar to that of an antipathetic dispersing agent, i. e. neutralize or discharge the stabilizing influences of the dispersing agents contained in the mixed suspensions. The most eil'ective coagulating agents are electrolytes and as such furnish in solution two types of ions: (at) one which may be absorbed and cause dispersion, and

(1)) one which tends to neutralize or discharge the dispersing ion and cause flocculation. When dispersed pigment particles are coflocculated from mixed suspensions by means of a coagulating agent which is an electrolyte, the flocculating power of that electrolyte may be considered as that concentration which ,iurnishes a sufficient quantity oi those ions which tend to neutralize not only'the original stabilizing ions of the disparsing agents but also those of the electrolyte itself.

Therefore an electrolyte with a strongly adsorbable dispersing or stablizing ion will necessarily require higher concentration in order to eilect coflocculation than an electrolyte with a weakly adsorbable stabilizing or dispersing ion.

Briefly stated, a coagulating agent should have a stabilizing ion which is only slightly adsorb:

able; that is, the influence of the ion having the same charge as that impinged upon the particles of the dispersed substances should be small, whereas that of the ilocculating or opposite ion should be great.

Although these considerations are useful in selecting coagulating agents and, to a certain extent, antipathetic dispersing agents for the practice of my invention I do not limit myself only to coagulating agents or antipathetic dispersing agents selected in accordance therewith.

The second of the two above noted methods of carrying out my invention is to choose the dispersing agents for the primary pigment and secondary pigment or pigments respectively, so that mutual cofiocculation occurs without the aid of a coagulating agent when the suspensions containing these dispersing agents are mixed together. Properly chosen dispersing agents will, when suspensions containing them are mixed together, nullify or mutually counteract the dispersing effect of each other and may be referred to as being antagonistic or antipathetic to each other.

It is practically impossible to list all the combinations of dispersing agents which may be employed in carrying out my invention according to this method.- Certain considerations are, however, helpful in arriving at a proper selection of antipathetic dispersing agents. For example, where a dispersion has been prepared by means of a dispersing agent furnishing preferentially adsorbed ions, an antipathetic dispersing agent will furnish ions capable of neutralizing or discharging the dispersing ions of the first dispersing agent. The ions of the antipathetic dispersing agent which fulfill this function are usually of opposite electrical potential. Consequently, acidic dispersing agents may be regarded as being antipathetic to basic dispersing agents and vice versa. For example; a mutual cofiocculation will result when a suspension of titanium dioxide, prepared by means of the acidic salt, aluminum chloride, is mixed with a suspension of barium sulfate prepared with the basic substance, sodium silicate.

In general, as will be readily ascertained from this description of my invention and particularly from the specific embodiments thereof, dispersion of the primary or secondary pigments may b effected by the use of only a small amount of dispersing agent. When it is desired to bring about the coflocculation of the composite pigments as a result of neutralizing or antipathetic properties oi the respective dispersing agents, it may be advantageous to use substantially stoichiometric proportion of the agents selected. However, if it be desired to coflocculate by means of a coagulant such consideration is not important.

After the pigment particles have been coiiocculated from the mixed suspensions they may be separated from the supernatant liquor by any suitable means such as decantation or filtration or both. The dispersing agents as well as the coagulating agents are thus practically completely removed. The cofiocculated pigment particles may then be washed to remove any residual soluble dispersing agent, coagulating agent, or reaction products resulting from an interaction between antipathetic dispersing agents, and then dried. In those cases where an insoluble dispersing agent had been used the small amount remaining in the pigment afterremoval of the supernatant liquor and washing will exert no detrimental effect on the quality of the product. When dried, coilocculated pigments prepared according to the methods of the present invention may be readily pulverized in order to render them suitable for use in the industrial arts.

There is obtained, as a result 01 my novel collocculation processes, an integration of particles of the primary and secondary pigments originally dispersed in which the particles are intimately associated in such relationship that,aiter washing, drying and pulverizing, they possess pigment properties which are comparable to those possessed by the coalesced composite pigments of the prior art. There is involved, I believe, in the integration resulting from my coflocculation processes an association as intimate and/or an aflinity between the primary pigment particles and those of the secondary pigment or pigments which is at least as strong as that resulting irom the comeclpitation and conjoint calcination methods of the prior art for the preparation of the so-called coalesced composite pigments. For these reasons I employ the term integrated" as descriptive of the association of pigment particles cofiocculated as above described.

In the Letters Patent to issue on this, the original application, I broadly claim the first of the two methods above described wherein dispersing agents are employed which are not antipathetic to one another and in which a coagulating agent is used for effecting coflocculation of the dispersed pigment particles. In addition to the broad claims to this process specific claims are included to the use of titanium dioxide and composite titanium dioxide pigments as the primary pigments and barium sulfate and basic carbonate white lead as the secondary pigments, to sodium silicate and lead chloride as dispersing agents, and

to magnesium sulfate as the coagulating agent, all

as will appear in the claims hereof.

In the Letters Patent No. 2,176,877, issued October 24, 1939, on application Serial No. 239,512 filed November 8, 1938, as a divisional application hereof, I have broadly claimed the second method above set forth wherein antipathetic dispersing agents are employed for the primary and secondary pigments respectively, and in which coflocculation of the dispersed pigment particles takes place upon simply mixing the dispersed suspensions. In addition to the broad claims to this process specific claims are included to the use of titanium dioxide, composite titanium dioxide pigments, and zinc sulfide as the primary pigments and barium sulfate, calcium sulfate, and basic carbonate white lead as the secondary pigments, to aluminum chloride, sodium silicate and hydrogen suiflde as dispersing agents, all as will appear in the claims thereof.

In the Letters Patent No. 2,176,876, issued October 24, 1939, on application Serial No. 239,511

'stantially an filed November 8, 1938, as a divisional application hereof the claims are restricted to the first method above set forth wherein zinc sulfide is employed as the primary pigment with claims specific thereto, in which the secondary pigment is barium sulfate, sodium silicate is the dispersing agent and magnesium sulfate is the coagulating agent.

It is to be specifically understood that no abandonment of any of the claims not presented in this, the original application, or in the two divisional applications above set forth is to be incurred by the order in which the Letters Patent hereon and on the said two divisional applications may issue or by the fact that all of the claims are not presented in a single patent, reservation being hereby specifically made to present the claims in this and in the two divisional applications as just above set forth.

In this, the original application, with the understanding and reservations above set forth, I now present specific examples of carrying out the vari ous processes herein above described including not only the method herein claimed but also the methods claimed in said divisional applications Serial No. 239,511, filed November 8, 1938, Patent No. 2,176,876, issued October 24, 1939, and Serial No. 239,512, filed November 8, 1938, Patent No. 2,176,877, issued October 24, 1939. It will be further understood, of course, that my invention is not in any way to be restricted to these specific examples as below given which are for illustrative, but not limitative, purposes.

EXAMPLE No. 1.-TI'rANxtm DIOXIDE-BARIUM SUL- rare Comrosrrn PIGMENT Two methods are given in which titanium dioxide pigment and barium sulfate are employed in the preparation of composite pigments of substantially similar proportions and possessing substantially the same pigment properties. A suitable titanium dioxide pigment is that which is obtainable in anhydrous, crystalline condition prepared, for example, according to U. 5. Pat enfs Nos. 1,288,863; 1,333,819 and 1,348,129. It may contain phosphorous compounds as described in U. S. Patent No. 1,412,027. Natural barytes which has been ground, purified, bleached and elutriated, thus assuring uniformity and fineness, is a satisfactory source for the barium sulfate. 0n the other hand, a blanc flxe having the same chuacteristics as the ground, purified and elu trlated barytes may also be used.

Method A.Coflocculation by use of antipathetic dispersing agents lbs. of the above described titanium dioxide pigment are milled in a suitable mill such as a porcelain ball-mill for about 2 hours with subequal weight of water and about 1% of its weight of aluminum chloride. 300 lbs. of barium sulfate, BaSO4. either ground natural barytes or blanc ilxe, selected as above described are milled in a similar manner for about 2 hours with about an equal weight of water and about A to per cent of sodium silicate, preferably of a ratio NazO to $10: of 1:4.

The two suspensions are then mixed in a suitable tank. Mlitual oofloeculation results through interaction of the aluminum chloride and sodium silicate. The coflocculated integrated pigment particles are then separated from the supernatant liquor, washed and dried, preferably at a temperature between lou C. After drying, the composite pigment is easily pulverized.

The pigment thus prepared is a composite consisting of approximately 25 parts of titanium dioxide and 75 parts of barium sulfate.

Method B.C'ofloccu1ation by means of a coagulating agent 100 lbs. of titanium dioxide similar to that used in Method (A) are milled for 2 hours with 4.5 lbs. of sodium silicate and about an equal weight of water. 300 lbs. of barium sulfate similar to that used in method (A) are separately dispersed by milling for about 2 hours with 9.0 lbs. of .sodium silicate and about an equal weight of water.

The two suspensions are then mixed. Since no coagulation will result from the use of the same dispersing agent for both primary and secondary pigments, 2.4 lbs. of magnesium sulfate in aqueous solution were added to bring about a cofiocculation and integration of the suspended titanium dioxide and barium sulfate. The integrated composite pigment is then treated as under Method (A) of this example.

The resulting composite pigment is similar to that obtained from the process given in method (A).

EXAMPLE No. 2.Zmc Summon-Barnum SULFATE PIGMENT Method A.Coflocculation by use of antipathetic dispersing agents 100 lbs. of commercial zinc sulfide pigment are milled for about 2 hours with about 35 gallons of water saturated with hydrogen sulfide, H25. 233 lbs. of barium sulfate similar to that employed in Example No. 1 are separately dispersed by milling for about 2 hours in 33 gallons of water in the presence of 2.66 lbs. of sodium silicate.

When the two solutions are mixed together coflocculation of the dispersed pigment particles occurs without the necessity of employing a coagulating agent.

The cofiocculated pigment particles are filtered, washed and dried at about 100 C., after which a pulverization may be employed.

Method B.-C0fl0ccu1ation by means of a. coagulating agent 100 lbs. of commercial zinc sulfide pigment are dispersed by milling for about 2 hours in 30 galions of water in the presence of 1.5 lbs. of sodium silicate. 233 lbs. of barium sulfate similar to that of Example No. 1 are milled with 33 gallons of water in the presence of 2.66 lbs. of sodium silicate. for about 2 hours. H r

The two dispersions are then mixed and about 2.4 lbs. of magnesium sulfate in aqueous solution are added to coflocculate the suspended particles of zinc sulfide and barium sulfate. The coflocculated pigment particles are treated as under method (A) of this example.

The products of both methods (A) and (B) of this example are integrated composite pigments comparable to lithopone of similar composition prepared by prior art methods.

EXAMPLE No. 3.Trmmuu DIOXIDE-BARKER! SUL- FATE-BASIC LEAD CARBONATE (lou'rosrrn Pronns'r Two methods are given for preparing a tertiary integrated composite pigment in which the primary pigment is, itself, a composite pigment dispersed, as a simple material, in one suspension. The primary pigment selected for this example was coprecipltated, mutually calcined composite titanium dioxide-barium sulfated pigment. The basic lead carbonate was obtained according to the well-known Dutch process corrosion of lead by acetic acid in the presence of decomposing organic matter.

Method A.-Coflocculation by use of antipathetic dispersing agents 100 lbs. of a composite pigment consisting of about 25% titanium dioxide and 75% barium sulfate are dispersed in 100 gallons of water by 20 are mixed. The cofiocculated pigments are filtered, washed, dried at about 110 0., and pul verized.

Method B.Cflocculation by means of a. coagulating agent 100 lbs. of the coprecipitated, mutually calcined titanium dioxide-barium sulfate composite pigment are dispersed by ball-milling for 3 hours with 100 gallons of water containing 0.5 lb. of sodium hydroxide. lead carbonate are dispersed by milling for 3 hours with 50 gallons of water containing 0.2 lb. of barium hydroxide. The two suspensions are mixed and the suspended pigment particles coflocculated by adding 0.78 lb. of 93% sulfuric acid to the mixed suspensions.

The coflocculated pigment particles are filtered, washed, dried at about 110 C., and pulverized. There is thus obtained an integrated composite pigment similar in composition and properties to that obtained under method (A') of this example.

EXAMPLE No. 4.TITANIUM DIOXIDE-BABIUM SUL- FATE-BASIC Luau CABBONATE Conrosrra PIGMENT This example illustrates the method of preparing a tertiary integrated composite pigment in which all three pigment components are separately dispersed. The titanium dioxide, since it possesses the best pigment properties is to be regarded as the primary pigment.

7 lbs. of titanium dioxide similar to that employed in Example No. l. are dispersed by ballmilling for 2 hours in an equal quantity of water containing about 0.2 lb., of sodium hydroxide. 25 lbs. of barium sulfate, either the natural barytes which has been treated as described under Example No. 1 or an equivalent blanc flxe, are dispersed by milling for 2 hours with a substantially equal weight of water containing 0.5 lb. of sodium silicate.

100 lbs. of basic lead carbonate, similar to that used in Example No. 3 are dispersed by ballmilling for 2 hours with approximately 100 gallons of water containing 1.0 lb. of sodium silicate.

The three separately prepared suspensions are then mixed. The suspended pigment particles of titanium dioxide, barium sulfate, and basic lead carbonate are ooflocculated by adding 8.0 lbs. of magnesium sulfate in the form of a 20% aqueous solution to the mixed suspensions.

The coflocculated pigment particles are then filtered, washed, dried at about 100 0., and pulverized.

The tertiary in ated composite pigment is Similarly, 100 lbs. of basic similar to that obtained from both methods (A) and (B) of Example No. 3.

It will be seen that my methods are admirably suited to the preparation of pigments of any desired predetermined proportions. In determining the desired proportions of primary and secondary pigments the use to which the composite pigment is to be put should be taken into consideration. If the requirements are such as to demand a pigment having a high tinting strength, good opacity, etc., a relatively larger amount of primary pigment will be used.

Furthermore, my coflocculation methods are not limited to the preparation of white composite pigments but are excellently adapted for the preparation of colored composite pigments.

It is accordingly possible to prepare a pigment consisting of two or more colored pigments of any desired color or tint, and it is equally possible to tint a white pigment with any desired tint. For example. if a dispersion of chrome yellow in lead chromate-lead sulfate pigment) be prepared and also one of Prussian blue (a ferric ferro cyanide) there will result on. coflocculation a green pigment of any desired shade depending on the relative proportions of chrome yellow and Prussian blue used. Thus, also, for example, a titanium dioxide pigment may be tinted a buff or light green or any other desired tint by subjecting it to a coflocculation process together with the desired quantity of a buff, or green. or other desired toner. Colored pigments prepared according to my cofiocculation methods are outstanding for their evenness of color and tone and when incorporated with vehicles to prepare surface coatings spread out without streaks or unevenness of color. Their uniform color renders them advantageous for use in other industrial arts as well.

Composite pigments prepared according to my coflocculation methods are preeminently adapted for use in surface coatings such as paints, enamels and lacquers. They are equally well adapted for the manufacture of opaque white or colored paper either by adding them to the paper as a heater addition or in other suitable ways. They are also useful in the manufacture of rubber goods such as white side walls for pneumatic tires, white or colored dress shields, bath curtains, overshoes, raincoats, and the like. In general they are excellently suited for use wherever a high quality white or colored pigment of great uniformity is required.

The foregoing detailed description has been given for clearness of understanding and no undue limitations should be deduced therefrom, but the appended claims should be construed as broadly as possible in view of the prior art.

I claim:

1. In the manufacture of composite pigments. the process which comprises dispersing a primary pigment in aqueous suspension by means of a rately-dispersing a secondary pigment by means 01 a small amount or a dispersing agent which is not antipathetic to the dispersing agent for said primary pigment, mixing the separatelydispersed suspensions, coflocculating the dispersed pigments by means of a coagulating agent, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverlzing the same.

3. A process for the manufacture of a composite titanium dioxide pigment which comprises dispersing calcined titanium dioxide pigmentin aqueous suspension by means of a small amount of a dispersing agent, separately dispersing a secondary pigment in aqueous suspension by means of a small amount 0! a dispersing agent which is not antipathetic to the dispersing agent for primary pigment, mixingthe separately-dispersed suspensions and mixing the separately-dispersed suspensions coflocculating the titanium dioxide and secondary pigment by means of a coagulating agent, separating the coilocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverizing the same.

4. A process i'or the manufacture of a composite titanium dioxide-barium sulfate pigment, which comprises dispersing calcined titanium dioxide pigment in aqueous suspension by means of a small amount 01' a dispersing agent, separately dispersing barium sulfate in aqueous suspension by means of a small. amount 01' a dispersing agent, which is not antipathetic to the dispersing agent for said titanium dioxide pigment, mixing the separately-dispersed suspensions and coflooculating the titanium dioxide and secondary pigment by means 01 a coagulating agent, separating the coflocculated pigments thus integrated from the supernatant liquor, and

washingdryingandpulveflzingthesame.

5. A process for the manufacture 01' a composite titanium dioxide-barium sulfate pigment, which comprises dispersing calcined crystalline titanium dioxide in aqueous suspension by means of a small amount of sodium silicate, separately dispersing barium sulfate in aqueous suspension by means of a small amount of sodium silicate, mixing the two suspensions, cofloccuiating the titanium dioxide and barius sulfate by means of magnesium sulfate, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing. drying and pulverizing the same. I

6. A process for the manufacture of a composite titanium dioxide-barium sulfate-basic lead carbonate pigment which comprises dispersing a titanium dioxide-barium sulfate pigment of which the titanium dioxide pigment portion consists of calcined titanium dioxide in aqueous suspension by means of a small amount of sodium silicate, separately dispersing basic lead carbonate in aqueous suspension by means of a small amount of lead chloride, coflocculating the titanium dioxide-barium sulfate pigment and basic lead carbonate by means of a small amount of magnesium sulfate, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverizing the same.

7. In a process for manufacturing a composite pigment by coflocculating separately-dispersed suspensions of pigments, the steps which consist in preparing the separately-dispersed suspensions of pigments by means of dispersing agents which are not antipathetic to each other, mixing together the said suspensions and coflocculating the dispersed pigments by means of a coagulating agent.

HUGH V. ALESSANDRONI. 0

CERTIFICATE OF CORRECTION.

Patent No 2,176, 87 5- October 21 1959.

HUGH V. ALESSANDRONI.

It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows 0nd column, line 75, for the word "absorbed" Page 2, secread adsorbed; page 6, first column, lines 19 and 20, claim j strike out "mixing the separately-dis persed suspensions"; and second column,

and that the said Letters Patent should be read with this correcbarium;

line 9, claim 5, for barius"read tion therein that the same may conform to the record or the case'in the Patent Office Signed end sealed this l2th.day of March, A. D. 191 0.

(Seal Henry Van 'Arsdale, Acting Commissioner of Patents.

rately-dispersing a secondary pigment by means 01 a small amount or a dispersing agent which is not antipathetic to the dispersing agent for said primary pigment, mixing the separatelydispersed suspensions, coflocculating the dispersed pigments by means of a coagulating agent, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverlzing the same.

3. A process for the manufacture of a composite titanium dioxide pigment which comprises dispersing calcined titanium dioxide pigmentin aqueous suspension by means of a small amount of a dispersing agent, separately dispersing a secondary pigment in aqueous suspension by means of a small amount 0! a dispersing agent which is not antipathetic to the dispersing agent for primary pigment, mixingthe separately-dispersed suspensions and mixing the separately-dispersed suspensions coflocculating the titanium dioxide and secondary pigment by means of a coagulating agent, separating the coilocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverizing the same.

4. A process i'or the manufacture of a composite titanium dioxide-barium sulfate pigment, which comprises dispersing calcined titanium dioxide pigment in aqueous suspension by means of a small amount 01' a dispersing agent, separately dispersing barium sulfate in aqueous suspension by means of a small. amount 01' a dispersing agent, which is not antipathetic to the dispersing agent for said titanium dioxide pigment, mixing the separately-dispersed suspensions and coflooculating the titanium dioxide and secondary pigment by means 01 a coagulating agent, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverizing the same.

5. A process for the manufacture 01' a composite titanium dioxide-barium sulfate pigment, which comprises dispersing calcined crystalline titanium dioxide in aqueous suspension by means of a small amount of sodium silicate, separately dispersing barium sulfate in aqueous suspension by means of a small amount of sodium silicate, mixing the two suspensions, cofloccuiating the titanium dioxide and barius sulfate by means of magnesium sulfate, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing. drying and pulverizing the same. I

6. A process for the manufacture of a composite titanium dioxide-barium sulfate-basic lead carbonate pigment which comprises dispersing a titanium dioxide-barium sulfate pigment of which the titanium dioxide pigment portion consists of calcined titanium dioxide in aqueous suspension by means of a small amount of sodium silicate, separately dispersing basic lead carbonate in aqueous suspension by means of a small amount of lead chloride, coflocculating the titanium dioxide-barium sulfate pigment and basic lead carbonate by means of a small amount of magnesium sulfate, separating the coflocculated pigments thus integrated from the supernatant liquor, and washing, drying and pulverizing the same.

7. In a process for manufacturing a composite pigment by coflocculating separately-dispersed suspensions of pigments, the steps which consist in preparing the separately-dispersed suspensions of pigments by means of dispersing agents which are not antipathetic to each other, mixing together the said suspensions and coflocculating the dispersed pigments by means of a coagulating agent.

HUGH V. ALESSANDRONI. 0

CERTIFICATE OF CORRECTION.

Patent No 2,176, 87 5- October 21 1959.

HUGH V. ALESSANDRONI.

It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows 0nd column, line 75, for the word "absorbed" Page 2, secread adsorbed; page 6, first column, lines 19 and 20, claim j strike out "mixing the separately-dis persed suspensions"; and second column,

and that the said Letters Patent should be read with this correcbarium;

line 9, claim 5, for barius"read tion therein that the same may conform to the record or the case'in the Patent Office Signed end sealed this l2th.day of March, A. D. 191 0.

(Seal Henry Van 'Arsdale, Acting Commissioner of Patents. 

